Process for the manufacture of the solid compound of hydrogen peroxide and urea



' Patented 2 rnocsss 'ron rm; MANUFACTURED! m 1 soup courousn or oxmn AND William a. me, mad. s.w.,ma

Sales ration of New ork Afiiliatesilnc... New york, a. x, a corps.-

g Hamstring. Application AW 8. 1988.. I

ewmms cLuG -sss)" afterv s parating said compound fromthe greater My invention relates to the art or process of preparing the well known, solid chemical comor procedure tor'such preparation.

Substantially four distinct methods have been hitherto available for-preparing said compound. The usual practice operates upon a moderately aqueous solution of the components,

concentrated either by chilling said solution to such temperapound of hydrogen peroxide and urea, and, particularly, to a .new method tures. below ordinary room temperatures, as correspond to extensive crystallization of the com-.

pound, continuing by; filtration in order to effect separation from the greater part of the solvent water. and further by drying; or by evapcrating a considerable amount of excess water.

from said solution, preferably under pressures lessthan ordinary atmospheric pressures. and at temperatures not exceedingerdinary atmospheric temperatures, continuing-by completion oi drylng. According to a third method, morerecent ly proposed, the compoundisto be formed under given conditions through the absorption by urea..,

, .as solid,}'of hydrogen peroxide, as vapor, from a current or other gases or vapors. According to a fourth method, likewise more recently proposed, the preparation of. the solid compound is to be accomplished in two steps; the-first, an interaction between solid urea and a restricted o 3 gen peroxide, in such a uniform. manner, attainable through fine subdivision of'the reacting sub-'- quantity of highly concentrated-aqueous hydrostances, that a moist mixture isnot, even tern-.- porarily produced, and yielding a solid intermeabout one-half the finally requisite peroxide content; and the second, interaction between tity of highly concentrated aqueous. hydrogen peroxide, following the treatment and conditions of the flrst step,i and yielding a'flnal product, which contains after drying almost the full peroxide content of the solid compound.

In order to render the solid compound suf flciently stable for undergoing without extensive decomposition all subsequent handling and neeessary storage, the distributed presence of small amounts of stabilizing substances. must be secured'in the product, and such stabilization has been hitherto accomplished byincluding said stabilizers 'flrst'with one or ,bothof the reseting substances before their interaction, or. second, with their aqueousintermixture before separation from excess sol ent water, or by incor- "said intermediate product and a restricted quan part-of the excess solvent water,or by some combination of two 'or-more of these stabilizing procedures. As stabilizing substances citric acid. salicylic acid, tannic, acid; succi'nic acid, phen- .acetine, methyl phthalate, benzoylecgonine, boric acid, sodium hydrogen sulfate, sodium'hydrogen.

phosphates, acid phosphates. P ymphosphates,

metaphosphat'es, starch, amylase; dextrine, gly'cosen. acetanilide, "hippuric' acid; A phenylglycerineether, orthomethoxyjlphenylglycerine smear-em 'zyl oxethylether, sugars, 'pyrophosphoric acid, water glass. llrotalbic acid, gumarabic, sodium tin have reconi-, or ale-hit erto denee of any de'- chloride and mended.

characteristics scribed methods. amtflrst. the liberate, purposive employment; -tempert itures substantially abov'e atmospheric temper--.

aturesLand, second, thev requirement .of appre- .ciable periods of treatment for the combined formation. isolation, and stablization of the solid compound of hydrogen. peroxideaud urea. Each 7 of said methods involves. consequently, one or Some more of several serious disadvantages. "methods entail prolonging" the interaction 01' the components, or oontinuationoilthelr intermixing in the presence or water, while large quantities of diluent materials. such as solvent. .water, or inert gases or vapors are being handled or removed: such anethods' tend-to subiect 'the' already formed product, or the original compo- I acute, or both. to by decomposition. One

method entallsapiurality of separate steps and product, which contains, after drying, n involves, ,in addition-stosaid losses by decomposition, an uneconomic repetition of handling and preemption-or apparatus. Another method entails a supplementary treatment of'the mother liquor from the separated solid com-' 40 pound, for the recovery of a considerable quan up to ic per cent or more molecular excess 01 hydrogen peroxide in some of the reaction sysof these methods, the losses lead to yields of product. or to peroxide strengths 02- product,"

fall considerablywshcrt of theoretical 5 mins said stabilizers .with the w d W".

I tity oi said compo d carried by the solvent water,,in order toav id waste. This same method entails-further a e rate treatment of the solid compound for com lemenofit s1 stabilization. Some methods entail diiiicultyinproperlycon; trolling physical and that'theflnal stabilized product may not, i m. form. Unless allowance for losses is generous,

which chemical 1 conditions throughout a considerable mass of materlaLso The existence of one or more oi these various disadvantages in the hitherto known processes for preparing the solid compound. of hydrogen peroxide and urea has been reflected in a high cost of product in relation to the costs tor the raw materials. Such conditions have in turn obstructed wide use of this long-known, extremely convenient and concentrated form of hydrogen peroxide.

Notwithstanding all previous experience of the more or less rapid decomposition, at tempera tures substantially above ordinary atmospheric temperatures, of hydrogen peroxide solutions and of hydrogemperoxide compounds, and notwith= standing all previous teaching in technical literature on the subject, I have found that the preparation of the solid compound oi hydrogen peroxide and urea can be accomplished easily and conveniently, with a substantially quantitative yield oi material, excellent both in strength and stability, in a single step of short duration, followed only by immediately subsequent crys= tallization and completion oi drying of the solid compound, when the reaction is caused to occur at temperatures substantially above ordinary at mospheric temperatures, in a substantially liquid reaction-mixture comprising urea and highly concentrated aqueous hydrogen peroxide, or" which the water content is so restricted as to sufiice only for: immediate and substantially complete liquefaction after inter-mixing for thepurpose or rapidly securing homogeneity by agita- I have found that my process of preparation can be rendered more perfect lay the inclusion, prior to crystallization, in said liquid reaction mixture, at temperatures substantially above or= dinary atmospheric temperatures, oi small quart titles oi certain stabilizing substances, hereinafter specified.

I have furthermore found that said stabilizing substances may he chosen for properties such that their employment in said liquid reaction mixture at temperatures substantially above ordinary atmospheric temperatures favors their subsequent rapid crystallization, together with that ofv the solid hydrogen peroxide-urea compound at temperatures appreciably above ordi-' nary atmospheric temperatures whereby they become distributed in a satisfactorily uniform manner throughout the mass of solid compound, and therefore become serviceable, without a special step for their incorporation therewith, for adequate'stabilization oi the solid compound during and after drying and during storage at ordinary atmospheric temperatures,

I have found that, in carrying out the prepare tion of said solid compound at temperatures considerably higher than ordinary atmospheric temperatures, the observance of certain precautions for avoidance of appreciable decomposition renders my process more perfect. These precautions are, first, the previously mentioned inclusion of stabilizing substances; second, the limitation of the highest temperatures reached in the reaction-mixture through adjustment and control of the temperatures of, the separate components before intermixing, and through selection of the concentrations of the reacting substances employed; third, the limitation oi the period substantially complete fluidity oi the mixture of the components so that said period shall be not longer than that required for rapid, yet thorough mixing and reaction; and, fourth, the initiation of rapid cooling and crystallization, immediately Ill assume after the period of mixing and reaction, for example, by pouring the hot fluid onto a cool surface, or by suitably spraying the hot liquidintc dry air.-

I have iound that the cooled solid product which is rapidly formed after the last step in the process hereinbeiore described is moist with a low water content, and further requires only completion of drying at ordinary atmospheric temperatures in order to prepare it for grinding and compression into tablets, or for other treatment, for the trade. 7

I have iouncl that the aforesaid adjustment oi maximum temperatures belowsuch temperatures as are unnecessarily and ha'rmfully elevated either locally or generally in the reaction-mis-:-= ture, and the aforesaid limitation of the period 01 substantially complete liquefaction at the tern perature selected for the thorough mixing and reaction oi the components, hydrogen peroxide and urea, can both be insured by previous separate heating or one or both components to speciflable temperatures substantially above ordinary atmospheric temperatures. have found that the process of dissolution liquefaction of the solid component, which is endothermic or absorptive or heat, can be substantially promoted by the heat developed during the chemical inter-- %tion "between thecornponents, which is exo thermic or line Live or I have found that these processes opposite ter justed to the concentrations he components in the resulting aqueous intermixture, and to the specifiable temperatures of separate, previous heating of one or both components, so effectively that the total heat available the system after intermixing shall be more than sufiicient for immediate, substantially complete liquefaction, at the temperature selected, whereby the supply of additional heat from source, and, a corresponding undesired e: n of the effective period of intermixing and reaction of the components at such temperatures, are rendered unnecessary More particularly, my invention comprehends the employment at temperatures substantially above ordinary atmospheric temperatures, of all those aqueous mixtures of hydrogen peroxide and, urea which contain less than 36 per cent water, equivalent closely to less than 3 moles of water 101' each mole of hydrogen peroxide or urea, and which comprise substantially equimolecular mixtures of hydrogen peroxide and urea, including not more than 3 per cent molecular excess of either component, and which are further characterized by the requirement of temperatures not lower than 37 degrees C. for equilibrium between the fluid mixture and minimal quantities of the solid phase. The systems or mixtures hereby defined comprise not less than 38.5 per cent urea, not less than 21.3 per cent hydrogen peroxide, not more than 36 per cent water, and correspond closely to the dissolution ofthe urea at the selected temperatures in not less than 37 per cent aqueous hydrogen peroxide.

Of these aqueous mixtures of hydrogen peroxide and urea hereinbefore defined I have found some examples more advantageous than others for preparing the solid compound of hydrogen peroxide and urea, according to the influence of various considerations hereinafter discussed upon the choice of optimum values for concentrations and temperatures.

I have'found particularly eflicient those examples in which the said mixture comprises, roughiy, 31-32 per oomhydrog n peroxide, sea-s per cent urea, 12.5-13 per cent water. Suchmixtures l co i 'espond substantially to the dissolution of a a slightly less than equimolecular quantity oi dr'y. solid urea in approximately '10 per cent hydrogen .peroxide and usually exhibit crystals at temperatures close to-70 degrees C. I

. -Ii' mixtures are employed which contain appreciably less than l2.5 per cent water, corre-.- sponding, tor-example, to the dissolution oi a slightly less than equimolecular quantity oi urea f in 80 per cent hydrogen peroxide, 1 have found thatthe full advantage of-my'process is not gained. This efle'ct is due flrstly. to the'higher temperatures to which one or both of the separate components must be previously heatedin order to insure substantially complete liquefaction immediately subsequent to the completed 'intermixing; a'nd,' secondly, to the higher-temtend to be adversely aflectedby theseiactors. It is true that the lower water-content oi the crystallized product, which corresponds to a water-content lower than 12.5 per cent of the reaction-mixture,-.iavors rapid and nearly complete crystallization upon cooling, andiaeilitatec completion or drying, and otheroperations upon the product, but these advantages are offset by the adverse influence oi the other factors cited;

If, on the other hand. mixtures are employed which contain appreciably more than 13 percent water, corresponding. for example to the dissolution oi a-slightly less than equimoiecular quantity oi urea in, say, per-cent hydrogen perox ide, Ihave ioun'd'that maximum efllciency of my invention is not'obtained because of the increased quantity of water in mixture. Subsequent crystallization is lessrdpid and less complete fora given degree of cooling, the consistency of the cooled crystalline masahas a tendency to be mushy or. paste-like,' due to the larger accumuiations or fluid accompaniment,--the material is consequentlyless' amenable to handlim.

and to subsequent drying operations. which therebyare rendered more complicated, as wellas more prolonged. comparative easeioi pre paring. hydrogen solutions containing less than 'wper cent hydrogen'pere the chic: advantage gained- ;-rrom: theiruse. at such solutions" not appreciably improve theec'onomy and regulation oivthe process. nor the yield.

and. stability oi-the' product, through the eiiect of such iactors as the lower requiredior separate heating of one or both'comtemperatures requiredior maintaining the completed intermixturerin a state of substantially complete liquefaction until ready for crystallization, and the lower temperatures the P ogress ,or crystallization.

- My invention further comprehends thestabillmixture of the components. of an'amount ot certain stabilizing substances not exceeding 3 per of generating in aqueous media a mild acidity 5 an physically, as substances solid and less than moderately soluble inaqueous media; at ordinary temperatures. '1 recommend orthophthalic acid,

the reaction-mixtures comprehendedin my inventionis not in all cases necessary for stabili-' zation of said mixtures at temperatures substantially above ordinary. atmospheric temperatures, vbut the regulation of the-physical and chemical conditions favoring stability within said mixtures is always rendered more perfect through the presence therein of such stabilizers. I rec- -ommend therefore their employment. The operp'eratures which are required for maintaining ative convenience of my process is well served the mixture in a condition of substantially com-. plete liquefactionuntil ready ior crystallization;

. The economy and regulation or the process. as

well'as the strength and stability of the product,

cation oi the crystallized and dried solid .com-

by the inclusion or such stabilizers with one or both of the reacting substances before interjMy invention further comprehends the stabilipound of hydrogen peroxide and urea by the reaction-mixtures at any time prior to.crystallization of the solid compound, and through crystallization of saidfstabilizers csether with crystallization oi the solid compound at tem- Deratures substantially above ordinary a'tmos-' pherio temperatures.- I point out particularly the absence in the previousnumerous and vari-.

.. pus recommendations of the prior art/tor the stabilimtion or the compound or hydrogen per-' 40 oxide and urea, either as solid or dissolved in aqueous media, of a comprehensive iormulation oi. the essential requirements (or such stabilizers -as are adapted equally for the stabilizationoi;

highly concentrated aqueous solutions of the said 'f compound, or its components. or both, at temperatures substantially above ordinary. atmos- .Pheric temperatures, and for stabilization 'oi' the 7 .solidcompound at ordinaryratinospheric'tem-i pefratures, and for the distributed incorporation not said stabilizers with said solid compound, independently oi a'separate or supplementary tre'at- [merit of said compound or or one or' both of its components for such incorporation. More particularly, I point out the novelty gandusemlness of my selection of stabilizers iorithjat combination orchemical and-physi l Properties, which is adapted simultancol y to chemical stabilization of the reaction-mixtures comprehended in my invention at temperamres substantially aboveponents previous to intermixing, and thelower ordinary atmospheric temperatures and of the -solld compound at ordinary ritmos'pheric tem-' peratures, and to proper. distribution or said stabilizers, without aispreciakle segregation. throughout the solid product by the physical reaction of rapid crystallizati iipherent in'mylid compound.

process of preparation or said A My invention further comprehends vthe limi-- tation of the somewhat variable highest ternperatures reached in the reaction-mixtures comprehended in my invention, and further. the" .limlt'ationot the period or inter-mixture oi'the' comp'onenta'hydrogen peroxide andurea, in said reaction-mixtures at temperatures substantially above ordinary atmospheric temperatures, cent by weight of thesolid product obtainedatter through a procedure for securing substantially i than ordinary atmospheric temperatures.

- requirement or substantially complete liquefaction in the reaction-mixtures comprehended in my invention immediately after the completion of intermixture is equally desirable, in order to accelerate and facilitate thorough mixing and distribution of the components, hydrogen perox crystallization of the solid compound. The gradual accomplishment of substantially com- 'ide and urea, and of the stabilizers, prior. to

piete liquefaction after intermlxing, for example,

through supply of heat to the reaction-mixture from an external source, constitutes less advantageous procedure, since such procedure prolongs-the period of intermixture at temperatures substantially above ordinary atmospheric temperatures, and involves local, temporary overheating above necessary temperatures. Through the procedure which consists of separate heatingof one or both components, hydrogen peroxide and urea, previously tointermixing, and of the reciprocal adjustment of their separate temperatures at the time of intermixing, the requirement of immediate and substantially complete liquefaction in the resulting reaction-mixture at temperatures substantially higher than ordinary atmospheric temperatures, and corresponding to the relatively high crystallization temperatures of the reaction-mixtures comprehended in my invention, is reconciled with the requirement for limitation of maximum temjustment of temperatures depends upon the con' centrations o! the reacting substances selected or available fortheprocess', and upon the procedure adopted, but said temperatures are readily speciflcable from data quickly obtainable in one or more trial experiments !or any givencombination of said concentrations and'procedure.

For purpose of exempliflcation therefore but without limiting the scope of my invention thereto, I describe a. process oi producing the solid compound of hydrogen peroxide and urea according to my method by examples, wherein parts signifyfparts by weight, as follows:

Example 1 128 parts of urea. are warmed with 4 parts of added ortho-phthalic acid to 95 d fl o the warm mixture at. 95 degrees C. are added 105.5 parts or 71.1 per cent aqueous hydrogen peroxide, containing. parts of hydrogen peroxide, equivalent to 1104 times the theoretical requirement, at a temperature of 108.5 degrees (3., attained in. previous separate warming. 75

There results immediately, upon adequate agitation and intermixing a clear, substantially fluid reaction-mixture at a maximum temperature 01' 75 degrees C., which'is poured in a fluid condition at 68.5 degrees C. after 3 minutes onto a cool surface for crystallization. Crystallization is immediate, and is completed in large part while the material is still warm.. The solid material is moist with'about 12.8 per cent water, which is rapidly removable at ordinary atmospheric pressures and at temperatures not exceeding ll degrees C. by a current of dry mr. The air dried product amounts to 5 pa s containing 34.9 p91 .cent hydrogen peroxide, and 1.25 per cent free phthalic acid. The yield of dried solid product amounts therefore to 99.3 per cent of the theoretical yield based upon the combined parts of u'reaand stabilizer, andihe hydrogen peroxide yield amounts to 97.8 per cent of the theoretical yield based upon the combined parts of urea and stabilizer, and to 94.2 per cent of the hydrogen peroxide employed. The stability of the solid product is very good, corresponding to a mean loss of 0.0075 gram hydrogen peroxide per gram per hour at 76.2 degrees (2., which is closely the stability of good, commercial grades 01 the product.

Example 2 theoretical requirement, at a temperature of -20 degrees C. There results immediately after intermixlng and agitation a clearysubstsntially fluid reaction-mixture'at a maximum temperature of 81 degrees C.,-which is poured in a fluid condition at 72.5 degrees (Letter 3 minutes onto a cool surface for crystallization. Crystallization is immediate, and is completed in large part.

while the material ls stlll warm .;-'1he solid material is moist with about 12.8, per cent water, which is rapidly removable under ordinary atmospheric pressures and -at temperatures not exceeding 41 degrees C. by a current of dry air.

The-airdried product amounts to 202.4 parts,

containing 35.1 percent hydrogen peroxide, and 1.06 .per cent tree phthalic acid. The. yield of dried solid product amounts flier-store to 99.2 per cent of the theoretical yield based upon the combined parts of urea and stabilizer, and the hydrogen peroxideyield amounts to 98.1 per cent of the theoretical yield based upon the-combined parts of urea and stabilizer, and to 93.91per cent 01' the hydrogen peroxide employed. Theistabil ity of the solidproduct is very good, corresponding to a mean loss of .0075 gram hydrogen peroxide per gram per hour at 76.2 degrees (3., which is closely the stability ofgood commercial grades 0! the product. 1

It is'possible further Within. or my invention tovary somewhat ths proportions of the diflerent ingredients! the temperatures em played; the periods during which materials are subjected to these temperaturespthe concentrations selected, as hereinbeiore. described; the nature, amountandftimeor addition or the substance or substances included for stabilizes tion; the temperature and agency employed for cooling the molten material; also the time, temperature and agency employed for drying the product; and other factors, according to such 5 considerations as the quality of the raw materials, and the desired characters of the product. For instance, atomization of. the hot fluid mixture of the components into turbulent, warm, dry

air may be employed, since cooling, crystallization and partial drying would occursimultanee iously, and the resultant finely divided product would be immediately adapted to further treatment; such as completion of drying, and/or com-- pression into tablets; 1 Y

I claim:

1. A process for the manufacturejof the solid chemical compound ofhydrogen peroxide and urea, which includes compounding a highly con-' centrate'd, aqueous mixture with not more than 36 per cent water,'and substantially equimolecular proportions ofhydrogen peroxide andurea, efl'ecting' substantially complete liquefaction di rectly after intermixing the components, andat centrated aqueous mixture with 'not'more than urea, not less than-21 .8 per cent hydrogen per oxide, eifeeting substantially complete liquefaction, directly afterv intermixing of the compo- 36 per cent water, not less than 38.5 per cent urea, not lessthan 21.3 per centhydrogen peroxide, effecting a' substantially completeliquefaction directly after intermixing of the compofnents, and at temperatures not lowerthant'l degrees C. or highertha'n temperatures involv- ,ing harmfully extensive decomposition, and there upon cooling to eflect crystallization throughout substantially the entire mass of said mixture. 3. A process-for the manufacture of-the solid chemical, compound of hydrogen peroxide and urea. which'includes compounding'a highly con- .rectly after intermixing of thecomponentsyand at temperatures substantially higher thanBPIf-Or and lower'than'\temperatures involving 'harmfully I extensive decomposition, and stabilizing said extensive decomposition, mixture by incorporation ce'ntrated aqueousmixture with not more than ula'r proportions of hydrogen peroxide and urea, eifecting illbstantially" complete jliquefacti'on ;di-- 1 mixture by incorporation therewith, at sometime prior to crystallization of the solid compound, of stabilizingsubstances whichare resistant to oxidation, mildlyacidic; and of less than moderate independent solubility inaqueous media at ordi nary temperatures,- in amounts not exceedingt .per cent. of the solid product thereafter obtained,,

and thereupon causing crystallization throughout substantially the entire mass of said .mixture'by 00 8.

.4. A process for the manufacture of the solid chemical compound of'hydrogen peroxide and 65 urea,- which includes compounding a highly con- .centrated aqueous mixture with not .more than 361p; cent water, and substantially equimolec- I -ular proportions of hydrogen peroxide and urea,

eifecting substantially completeliquefaction iii rectly after intermixin'g' of the components, and at temperatures substantiallyhigher than 37 C. and lower than temperaturesinvolving harmfully and stabilizing said i 38 per cent water, and substantially equimolec .said mixture byicooling.

components, and prior to-their-intermixing, of substances. which are resistant to oxidation, mildly acidic and of less than moderate independent solubility in aqueous media at ordinary temperatures, in amounts not exceeding 8 per cent 1 of the solid product thereafter obtained, and

thereupon causing crystallization throughout substantially the entire ,massrof said mixture 'by cooling.

,5. A prouss fOl' the manufacture of thesolid chemical compound of hydrogen peroxide and urea, which includes compounding a highly con-l centrated' aqueous mixture with .not more than 36 per cent water, not less than 38.5 per cent I urea, not. less than 21.8,per centhydrogen peroxide, eflecting substantially complete liquefac-' tion directly after intermixing of the components, and at temperatures not lower than 3'1 degrees C. or higher than temperatures involving harmfully extensive decomposition, and stabilizing said mixture by incorporation therewith, at some prior time .to crystallization of the solid compound, of substances which are resistant to pxidation, mildly acidic, and of less than moderate independent solubilityin aqueous mediaat ordinary atmospheric temperatures, in amounts not exceeding 3 per cent of the solid product thereafter obtained, and-thereupon causing crystallizatiomthroughout substantially entire mass of said mixture by cooling.

6. A process for the manufacture of the solid j chemical compound of hydrogen peroxide. and urea, which includes compounding ahighly concentrated aqueous mixture with not more than 86 per cent water, notless than 38.5 per cent 'nents, and at temperatures not lower than 37 degrees C; or higher than temperatures involving" 1 barmfully extensive decomposition, and stabilizing said mixture by incorporation with at least one of the components, and prior to theirintermixing, of substances'which are resistant to oxi-,

dation, mildly acidic, and of less than moderate independent solubility in aqueous media at oralafter obtained, and thereupon causing crystallization throughout suh'stantiallythe entire mass.

of said mixture by cooling.-

q .7. A process for the manufacture of-the solid -chemical compound of' hydrogen peroxide" and urea, which includes-compounding a highly con-,

centrated aqueous mixture with not more than 36 per' cent water,- and 'substantially-equimolec ular proportions of hydrogen peroxide andurea,

effecting substantially complete liquefaction directly ai'terintermixing of the components, and f at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition, and providing for ultimate stabilization of the solid compound by incorporation with said mixture, at some time prior to crystallizationof said solid compoundmf solid stabilizing substances which are resistant to oxidation, mildly acidic. and of less thanmoderate independent solubility in aqueous media at ordiparyatmospheric temperatures, in amounts not exceeding 3 percent ofthesOlid product thereafter obtained, and thereupon causing crystallitzation throughout substantially the entire mass of 8.; A; process with at least one of the chemical compound of hydrogen peroxide and v urea, which includes compounding a highly @0111 centrated aqueous mixture with not more than 36 per cent water, not less than 38.5 per cent urea, not less than 21.3 per cent hydrogen peroxide, effecting substantially complete liquefactiorl directly after intermixing oi the components, and at temperatures not lower than 37 degrees C. or higher than temperatures involving harmfully extensive decomposition, and n zovld ing for ultimate stabilization of the solid compound by incorporation with said mixture, at some time prior to crystallization of sold solid compound, of solid stabilizing substances which are resistant to oxidation, mildly acidic, and of less than moderate independent solubility in aqueous media at ordinary atmospheric temperatures, in amounts not exceeding 3 per cent of the solid product thereafter obtained, and thereupon causing crystallization through substantially the entire mass of said mixture by cooling.

9. A process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly con= centrated, aqueous mixture with not more than 36 per cent water, and substantially new ular proportions of hydrogen peroxide and urea, and securing substantially complete liquefaction immediately after intermixing of the components and at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition through heat partly derived from a scparate'w if of at least one of the components, prior to their in= termixing, to temperatures substantially higher than ordinary atmospheric temneratures, and thereupon causing crystallization throughout sub-- stantially the entire mass of said mixture by cooling. I

10. The process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly concentrated aqueous mixutre of hydrogen per= oxide and urea wherein water content is limited to not substantially more than 36%, effecting a substantially complete liquefaction directly after intermixing oi the componentaanzl at temperatures substantially higher than 37-- C. and lower than temperatures involving harmfully sive decomposition,- and thereupon oooling'tocilect crystallization throughout substantially the entire mass of said mixture. l

11. The process for the manufacture of the solid chemical compound of hydrogen peroxide and tires, which includes compounding a highly concentrated aqueous mixture of hydrogen peroxide and ureagwherein water content is limited to not substantially more than 36%, effecting a liquefaction directly after intermixing. of the components, and at temperatures not lower than 3! degrees C. or higher then temperatures involving harmfully extensive decompomtlon, and

thereupon effecting crystallization throughout substantially the entire massof said.

12. The process for the 'manufactm-c of the solid chemical compound of hydrogenfneroxldc and urea, which includes compolm ms Q highly concentrated aqueous mixture of hydrogen peroxide and urea. wherein water content is limited to not substantially more than 38%, effecting on intermlxlng-and liquefaction at temperatures substantially higher than ,3? 0.; and; lower than temperatures involving harmfully olt n'sivo decomposition, and thereupon eifecting-u solidifl-i cation oi the compound of" the 'two components. 13. The process for the oilv the ascents solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly concentrated aqueousznixture of hydrogen peroxide and urea wherein water content is limited to not substantially more than 36%, and effecting an intermixing and liquefaction at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition.

is. The process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly concentrated aqueous mixture of hydrogen peroxide and urea wherein water content is limited to not substantially more than 36%. effecting an interrnlxing and liquefaction. of said components at temperatures substantially higher than 37" C. and lower than temperatures involving harmiully extensive decomposition and stabilizing said mixture by incorporation therewith, at some time prior to crystallization of the'solid compound, oi stabilizing substances which are resistant to oxi dation, mildly acidic, and of less than moderate independent solubility in aqueous media at orcli= nary temperatures. 15. The process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly concentrated aqueous mixture of hydrogen peroxide and urea wherein water content is limited to not substantially more than 36%, eifecting a liquefaction at temperatures substantially higher than 37 C. and lower than temperatures involvlug harmfully extensive decomposition and stabilizing said mixture by incorporation of orthophthalic acid therewith, at some time prior to crystallization of the solid compdund.

16. A process for the manufactureof the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly concentrated aqueous mixture with not more than 36 per cent water, not less than 38.5 per cent urea, not less than 21.3 percent hydrogen peroxide, and securing substantially complete liquefaction immediately after. intermixing of the components and at temperatures not lower than 37 degrees C. or higher than temperatures involving harmfully extensive through heat partly derived from a separate warming of at least one of the components, prior to their intermixing, to temperatures substantially higher than ordinary atmospheric temperchines, and v thereuponcausing crystallization throughout substantially the entire mess of said mixture by cooling.

17. A process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly concentrated, aqueous'mixture of hydrogen peroxidle and urea wherein water content is limited to not substantially more than 36%,eflecting substantially complete liquefaction directly after inte of the components, and at temper atures substantially'highcr than}? Ciand lower than temperatures lnvolvingrharmfully' extensive decomposition, and thereuponyeifectlng crystallization throughout substantially the entire mass of the said mixture;

18. A process for the manufacture of the solid chemical compound ofhydrogen peroxide andv urea, which includes compounding ahighly condecomposition rectly after lntermixing of the components, and at temperatures substantially higher than 37 C.

and lower than temperatures involving harmfully extensive decomposition, and stabilizing said mixture by incorporation therewith, at some time prior to crystallization of the solid compound, of orthophthalic acid, in amounts not exceeding 3 per cent of the solid product thereafter obtained,fand thereupon causing crystallization throughout substantially the entire mass of said mixture by cooling.

19. A process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding a highly'concentrated aqueous mixture with not more than 36 per cent water, and substantially equimolecular proportions of hydrogen peroxide and urea, effecting-substantially complete liquefaction directly after intermixing of the components, and

at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition, and stabilizing said mixture, and simultaneously providing for ultimate stabilization of the solid compound, by in-- corporation with at least one of the components, and prior to their intermixing, of orthophthalic acid in amounts not exceeding 3 per cent of the solid product thereafter obtained, and thereupon causing crystallization throughout substantially the entire mass of said mixture by cooling.

20. The process for the manufacture of the solid chemical compound of hydrogenperoxide and urea, which includes compounding an aqueous mixture of hydrogen peroxide and urea wherein the water content is not materially greater than 36%, the solution being of such high concentration that complete liquefaction subsists therein only at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition.

21. The process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding an aqueous mixture of substantially equimolecular quantitles of hydrogen peroxide and urea wherein the water content is not materially greater than 36%, the solution being of such high concentration that subsequently to complete liquefaction crystallization begins at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition.

22. The process for the manufacture of the solid chemical compound of hydrogen peroxide I and urea, which includes compounding an aqueous mixture of hydrogen peroxide and urea wherein the water content is not materially greater than 36%, the solution being of such high concentration that after intermixing of the components complete liquefaction is possible only at temperatures substantially higher than 37 C. and lower than temperatures involving harmfully extensive decomposition.

23. The process for the manufacture of the solid chemical compound of hydrogen peroxide and urea, which includes compounding an aqueous mixture of substantially equimolecular quantities of hydrogen peroxide and urea wherein the water content is not materially greater than36%, the solution being of such high concentration that after complete liquefaction and intermixing of the components crystallization begins at tem 5 peratures substantially higher than 37 C. and

lower than temperatures involving harmfully extensive decomposition.

WILLIAM EQ'MORGAN. 

